U.S. patent number 3,925,205 [Application Number 04/838,613] was granted by the patent office on 1975-12-09 for method of separating solids suspended in a liquid.
Invention is credited to Vaughan Reynell Sparham.
United States Patent |
3,925,205 |
Sparham |
December 9, 1975 |
Method of separating solids suspended in a liquid
Abstract
Colloidal or gelatinous solids suspended in a liquid, such as
sewage, are separated by passing the liquid through a labyrinth of
eddy-forming surfaces in series with a sheet perforate member. The
labyrinth may be formed from plate-like or tube-like members
arranged within a vessel having an inlet and an outlet for the
liquid. The members have eddy forming surfaces and are arranged to
form a labyrinth of passages through which the liquid must pass
preferably in an upward direction, when flowing from the inlet to
the outlet. The plate-like or tube-like members may have an
undulating cross-section or ribbed walls to provide the
eddy-forming surfaces. The labyrinth is preferably on the
downstream side of the sheet perforate member.
Inventors: |
Sparham; Vaughan Reynell (Great
Budworth, Northwich, Cheshire, EN) |
Family
ID: |
25277586 |
Appl.
No.: |
04/838,613 |
Filed: |
July 2, 1969 |
Current U.S.
Class: |
210/802; 210/521;
210/522 |
Current CPC
Class: |
B01D
21/0075 (20130101); B01D 21/02 (20130101); B01D
21/0051 (20130101); B01D 21/2416 (20130101); B01D
21/0003 (20130101); B01D 21/2405 (20130101); B01D
21/0039 (20130101) |
Current International
Class: |
B01D
21/00 (20060101); B01D 021/00 () |
Field of
Search: |
;210/73,84,521,522 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
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|
|
|
|
|
|
994,118 |
|
Nov 1951 |
|
FR |
|
13,996 |
|
Oct 1887 |
|
UK |
|
Primary Examiner: Adee; John
Claims
I claim:
1. An apparatus for reducing the solids content of a liquid phase
such as sewage works effluent containing colloidal or gelatinous
solids suspended therein, said apparatus comprising in combination,
a sedimentation tank having an inlet and an outlet, wall means
defining a separate chamber within the upper portion of said tank,
a sheet perforate member mounted in a substantially horizontal
position within said tank in vertically spaced relation to the
bottom wall thereof and defining the bottom wall of said chamber,
said outlet being located within said chamber whereby liquid
flowing from said inlet to said outlet must pass upwardly through
said sheet perforate member, and means defining a labyrinth mounted
within said separate chamber between said sheet perforate member
and said outlet whereby a liquid flowing from said sheet perforate
member to said outlet must flow through said labyrinth, said means
defining said labyrinth including a plurality of members mounted
within said chamber and cooperating to define a plurality of fluid
passages through which the liquid flows, said members having a
plurality of rugosities thereon extending generally across the
direction of flow for forming eddy currents in liquid flowing
through said passages to thereby promote cavity sedimentation and
adsorption of the solids from the liquid.
2. An apparatus as claimed in claim 1 in which the passages are
inclined to one another.
3. An apparatus as claimed in claim 1 in which the passages are
inclined with respect to the walls of the tank.
4. An apparatus as claimed in claim 1 in which the labyrinth is
arranged so that when liquid flows through the tank from the inlet
to the outlet, it passes through the labyrinth in a generally
upward direction.
5. The apparatus as defined in claim 1 wherein said plurality of
members comprises a plurality of plate-like members mounted in
side-by-side relation and wherein at least alternate ones of said
plate-like members have undulating cross sections.
6. An apparatus as claimed in claim 5 in which the plate-like and
tube-like members of the labyrinth are secured together to form
made-up units having a plurality of passages therein for the
liquid.
7. The apparatus as defined in claim 1 wherein said plurality of
members are elongated tube-like elements.
8. The apparatus defined in claim 7 wherein said tube-like elements
have undulating cross sections.
9. In an apparatus for removing suspended solids from a liquid,
said apparatus including a sedimentation tank having an inlet and
an outlet, a liquid-solids separation device positioned within said
tank and having means defining a plurality of fluid passages
arranged in closely spaced relation, and means directing the liquid
through said passages in its path from said inlet to said outlet,
the improvement wherein said means defining said plurality of fluid
passages comprises a plurality of plate-like members positioned in
side-by-side relation, said plate-like members having
longitudinally extending undulations formed therein to define said
fluid passages, and a plurality of surface discontinuities in the
form of a plurality of rugosities formed in said plate-like members
spaced along said passages producing a non-uniform cross section
along the length of said fluid passages, said surface
discontinuities being capable of producing eddy currents within
said fluid passages at flow rates therethrough in the low range of
laminar flow to thereby produce separation of the suspended solids
by cavity sedimentation and adsorption onto the surface of said
fluid passages.
10. The apparatus defined in claim 9 wherein said plate-like
members are secured together with the longitudinal undulations of
alternate plate-like members being disposed at an angle with
respect to one another.
11. In the operation of a system for reducing the solids content of
a liquid colloidal solids suspended therein, including an upward
flow sedimentation tank having an inlet and an outlet, a
liquid-solids separation device having a plurality of fluid
passages extending therethrough positioned within the tank, and
means directing the liquid through the passages in said device in
the liquid's path from the inlet to the outlet, the method
comprising the steps of flowing said liquid through a sheet
perforate member at a rate within the low range of laminar flow to
produce a fluidized bed of flocculated particles on the downstream
side of said sheet perforate member, flowing said liquid through
said separation device at a flow rate in the low range of laminar
flow within said fluid passages, and creating eddy currents in said
liquid while passing through said fluid passages to produce cavity
sedimentation and adsorption on the surface of said fluid
passages.
12. The method defined in claim 11 wherein said sheet perforate
member is positioned upstream from said separation device in said
sedimentation tank.
13. The method defined in claim 11, wherein said separation device
is positioned above said sheet perforate member, and wherein said
liquid is caused to flow upward through said sheet perforate member
then upward through said separation device.
14. The method defined in claim 13 wherein said liquid is sewage,
works effluent.
Description
This invention relates to the flocculation and clarification of
waters containing organic or inorganic impurities.
The suspended solids occurring in waste waters that have been
subject to purification by a process of biological oxidation may
contain as much as 300 parts per million of organic matter. Again,
the waters emerging from the preparation of coal and minerals can
contain sufficient fine particles in suspension to render these
waters unfit for direct discharge to natural water courses.
Effluents from these processes normally contain suspended solids
which are, in a large proportion, separated from the water phase by
simple sedimentation. Separation by this means, however, is seldom
complete, and a proportion which may vary between 30 and 1500 parts
per million according to the nature of the suspended solids may
pass out with the final effluent to the receiving stream or water
course. This is undesirable since these solids become attached to
or deposited on live plants on the bed of a stream inhibiting
photosynthesis and may even interfere with the free flow of the
stream due to silting up in areas of low flow velocities. It is
also possible that such suspended solids, may, in certain
circumstances, constitute a loss of valuable material.
The permissible limits of suspended solids specified in Federal
bye-laws has been based largely on the Royal Commission Standard of
Great Britain of 30 parts per million but increasingly lower
limits, such as 10 parts per million are being enforced. Among the
various methods of improving the quality of effluents in respect of
their suspended solids content are the following:
Where an adequate area of grassland on suitable soil is available,
substantial removal of residual solids is effected by distribution
of the effluent over the surface of the land so that it finally
reaches the stream after a proportion of suspended solids has been
adsorbed onto the leaf and stem surfaces of grass and other plants,
and also a certain amount of filtration through the soil.
Another method employed has been to pass the effluent through
micro-strainers before discharge. Micro-strainers consist
essentially of woven wire gauze having very fine apertures from 5
microns upwards to say 100 microns, such apertures being of the
same order of magnitude as the solids to be retained. For dealing
with humus particles from sewage purification aperatures of about
35 microns are employed. Necessarily, they must be made of very
fine wires and thus are relatively delicate and easily damaged.
They are also expensive.
In operation the solids retained by micro-strainers must frequently
be cleaned off to avoid blinding and suitable arrangements are made
to effect this.
Recently what are termed "upward flow clarifiers" known also in the
U.K. as "Banks Filters" have come into use for a similar purpose.
They consist of a conventional sedimentation tank within which a
bed of gravel of suitable grading, e.g. 1/4 to 3/8 inches, often 6
inches deep, is supported by a horizontal perforated floor in such
a position that liquor introduced below the perforated member
passes up through the gravel bed and thence to an outlet weir.
Reduction of suspended solids content in the final effluent to 10
parts per million or less can be achieved when operated under
optimum conditions. Mechanical coagulation of the residual solids
is said to occur during passage through the gravel, and the flocs
so formed lodge in the interstitial spaces of the gravel or settle
on its surface. The rate of flow through the bed is restricted
preferably to 10-15 galls/per Sq. ft./hr. and as in consequence
compression of the formed flocs is minimal, the bed remains
permeable for comparatively long periods, though from time to time
when the head loss approximates to about 1 inch, the accumulated
solids are removed by backwashing in known manner. These beds may
be mounted suitably either in the usual final sedimentation tank
itself, or in separate tanks. The perforate floor of the bed must
be of adequate strength to support the weight of the gravel which
may have to span a considerable area. The perforations in the floor
must be smaller than the lower sizes of gravel, e.g. with gravel
graded 1/4 to 3/8 inch perforations with a maximum dimension in one
direction of 3/16 inch are suitable.
It is said that the action of these gravel- or pebble-bed
clarifiers is a combination of flocculation, cavity sedimentation,
and adsorbtion. All three of these effects are in part due to the
acceleration of the flow of water passing through the interstices
of the gravel bed. Subsequent deceleration combined with the
variations of flow within the voids among the pebbles gives rise to
flocculation of the small particles which will either come to rest
in cavities amongst the pebbles in the bed or alternatively escape
to the upper surface of the bed where the reduced velocity of flow
will permit the newly-formed larger flocs to settle back onto the
surface of the bed.
According to the present invention there is provided a method of
separating colloidal or gelatinous suspended solids in a liquid
phase that comprises passing the liquid through a labyrinth of
eddy-forming surfaces in series with a sheet perforate member.
These surfaces may be made from, for example, (1) polyvinyl
chloride, (2) resin-bonded fibrous materials, (3) suitably prepared
metals, (4) linoleum, (5) timber, (6) asbestos sheets, (7) rubber,
(8) cork and (9) ceramics.
The invention is useful to the sewage disposal art and may also be
used in solids/liquid separation wherever it is required to remove
similar small suspended particles from the liquid.
The eddy forming surfaces may in general be the surfaces of
elements arranged to form the labyrinth, the arrangement being such
that the liquid passes through passages formed between the
elements. The passages preferably form zig-zag or non-linear paths
through the labyrinth. The direction of flow in relation to
gravitational forces can be arranged to suit the type of solids in
suspension to be separated from the liquid phase.
The invention includes apparatus for reducing the solids content of
a liquid phase containing colloidal or gelatinous suspended solids
which comprises a vessel, such as a sedimentation tank, having an
inlet and an outlet for the liquid, and a labyrinth having
eddy-forming surfaces arranged in the vessel so that when liquid
flows through the vessel from the inlet to the outlet it must pass
through the passages in the labyrinth.
The labyrinth may be formed from closely spaced plate-like or
tube-like members or elements which may be metallic or
non-metallic, e.g. they may be made from any of the materials (1)
to (9) indicated above.
The plate-like or tube-like members may have an undulating
cross-section and may also have ribbed walls. The plate-like or
tube-like members of the labyrinth may be secured together to form
made-up units having a plurality of passages therein for the
liquid. The passages may be inclined to one another and/or to the
walls of the vessel and may be of constant or variable
cross-section. Preferably, the labyrinth is arranged so that when
liquid flows through the vessel from the inlet to the outlet, it
passes through the labyrinth in a generally upward direction.
As indicated above, a sheet perforate member is arranged in series
with the labyrinth so that when liquid flows from the inlet to the
outlet, it also passes through the sheet perforate member.
Preferably the labyrinth is on the downstream side of the sheet
perforate member, that is to say liquid flowing through the vessel
from the inlet to the outlet flows first through the sheet
perforate member and then through the labyrinth. A sedimentation
tank may be provided having a compartment positioned close to the
top of the tank in such a way that liquid fed into the tank must
pass upwardly through the compartment before it can pass out of the
tank. By filling the compartment with the labyrinth e.g. the
assembly of elements, the liquid can be clarified and a large
proportion of the small particles can be retained on the walls and
among the cavities in the labyrinth. In addition, as with the
"Banks Filter", the labyrinth may be arranged in a tank separate
from a sedimentation tank.
Alternatively, the labyrinth may be provided in a vertical wall
positioned in a tank into which sewage effluent can be fed. The
labyrinth is positioned relatively close to one of the walls and
the wall containing the labyrinth is positioned so that sewage must
flow through a perforate member before it can leave the tank. This
embodiment may be modified by sloping the labyrinth from the
vertical or horizontal. This sloping of the labyrinth will in some
cases enhance the retention of fine particles due to gravitational
forces by modification of the eddy current flow pattern.
Means may be provided to regulate the flow of liquid from the
outlet of the vessel. The outlet may thus be in the form of a weir
provided with a decanting tray of a selected length for regulating
the flow of liquid. The liquid may flow over the rim of the
decanting tray or the rim may be v-notched or castellated or the
sides of the tray may be perforated to allow liquid to pass from
the vessel into the tray at the outlet. Alternatively, the outlet
may be provided with multiple offtakes. Such arrangements permit
control of the weir speed and/or length of draw at the outlet or
outlets of the vessel.
The efficiency of the invention can be augmented by the addition of
coagulants or by the application of a suitable electrical potential
where the labyrinth is constructed of a conducting material,
provided that suitable insulation is arranged.
The effectiveness of an eddy flow separator must be considered in
relation to overall tank design. Small particle separation is
normally enhanced by passing a paddle slowly through turbid water.
The eddy current separator provides a static paddle through which
the water and certainly some of the suspended matter passes. It is
therefore better that the design of the eddy current separator be
considered in terms of the mechanics of flocculation, and the
effect of this invention is to alter the hydraulics of a
conventional sedimentation tank. A sedimentation tank for final
settlement at a sewage works (where tertiary treatment is
envisaged) must be considered in terms of surface/overflow ratio.
The introduction of an eddy current separator into a sedimentation
tank somewhat alters the hydraulic behaviour of the tank. The
outlet from the tank is no longer in direct communication with its
base. It is well known that wherever streamlines develop they will
entrain solids with them. Consequently, the paths of fine particles
may be modified by the presence of the separator before actually
entering the labyrinth, due to the slight resistance to flow that
will develop immediately prior to the passage of the liquid through
the labyrinth. It now becomes clear that the effect of an eddy
current separator is both to regulate flow patterns and also to
create suitable eddy formation for the retention of fine particles
within its interstices.
The instability of floc blankets in upward flow sedimentation tanks
is a well known phenomenon. The eddy current separator will also
act as a stabiliser for these floc blankets.
The invention will now be further described by way of example with
reference to the accompanying drawings in which:
Each of FIGS. 1 and 2 is a side view of a pilot apparatus for
sewage clarification,
Each of FIGS. 3 to 7 is a perspective view of labyrinth-forming
elements for the apparatus of FIGS. 1 and 2,
FIG. 8 is a side view of a full scale apparatus for sewage
clarification and
FIG. 9 is a plan view of part of the apparatus shown in FIG. 8.
In each of FIGS. 1 and 2, a tank 10 is provided with an inlet 11
and an outlet 12 between which are a sheet perforate member 13 and
a labyrinth generally indicated by 14. In FIG. 1, the labyrinth 14
rests on the perforate member 13 but in FIG. 2, there is a space
between the member 13 and the base of the labyrinth 14. Liquid
passing through the apparatus of FIG. 1 or FIG. 2 from the inlet 11
to the outlet 12 flows upwards in the tank 10 through the perforate
member 13 and then through the labyrinth 14.
The labyrinth 14 may consist of tubes of any desired cross section,
such as the tubes of hexagonal section shown in FIG. 3 or the tubes
of circular section shown in FIG. 4, arranged so that the liquid
flows upwards through the tubes, which have ribs or indentations
15. Alternatively, the labyrinth 14 may consist of undulating
plates, such as those shown in FIGS. 5 and 6, arranged so that the
liquid flows upwards between the plates, which have indentations or
rugosities 16 and 17 respectively extending generally across the
direction of flow along the plates. The edges 18 may be at the top
of the labyrinth.
FIG. 7 shows a labyrinth in the form of a complete unit built up
from plates 19 and 20, only two of which are shown in FIG. 7 for
the sake of clarity, the rest of the unit being indicated by
chain-dotted lines. The unit is built up of alternating plates 19
and 20. The plates are provided with angular corrugations, the
peaks and valleys of the corrugations of the plate 19 running
upwards to the left of the figure and the peaks and valleys of the
plate 20 running upwards to the right of the figure. The entire
surfaces of each plate are covered with rugosities or ribs 21. When
the unit is positioned in the tank 10, the side 22 is approximately
vertical.
In FIGS. 8 and 9, a tank 23 has an inlet weir 24 and an outlet weir
25 communicating with an outlet channel 26. The tank 23 is also
provided with a closable outlet 27. A compartment 28 is located in
the tank 23 and has one wall abutting the weir 25. The base of the
compartment 28 is a sheet perforate member 29 which is shown
horizontal, but may if desired be inclined. The compartment is
shown filled with a labyrinth of eddy-forming plates 30 which may
be as shown in FIGS. 5 to 7, but tubes may be used instead. A
decanting tray 31 provided with holes 32 communicates at one end
with the weir 25. The direction of flow of the liquid through the
tank 23, compartment 28 and decanting tray 31 is indicated by the
arrows.
Five trials were carried out on upward flow clarification of the
final effluent from a sewage disposal works using the apparatus of
FIG. 1 except that in some of the trials, the perforate member or
the labyrinth was omitted as indicated below. In all cases the
labyrinth was formed from a material of the plastics class and the
structure of the labyrinth was as indicated below. In the tables
below "p.p.m." stands for parts per million. For all five trials a
constant flow of 20 gls/ft..sup.2 /hr. was maintained. The effluent
was taken from the outlet channel of a Dortmund humus tank.
Trial A
Labyrinth of FIG. 7 without perforate member.
______________________________________ Input Output % Hours run
Solids p.p.m. Solids p.p.m. Reduction
______________________________________ 2 48 13.2 72.5 18 37.6 9.6
74.2 ______________________________________
Trial B
0.25 mm. wedge wire perforate member plus labyrinth of FIG. 7.
______________________________________ Input Output % Hours run
Solids p.p.m. Solids p.p.m. Reduction
______________________________________ 3 40.2 3.1 92.3 5 43.1 3.0
93.0 8 46.0 3.1 93.2 ______________________________________
Trial C
0.25 mm. wedge wire perforate member only. No labyrinth.
______________________________________ Input Output % Hours run
Solids p.p.m. Solids p.p.m. Reduction
______________________________________ 2 31.2 7.6 75.6 4 38.4 8.4
78.1 6 40.0 16.0 60.0 8 41.2 13.4 67.5
______________________________________
Trial D
Labyrinth formed from elements of FIG. 6. No perforate member.
______________________________________ Input Output % Hours run
Solids p.p.m. Solids p.p.m. Reduction
______________________________________ 2 34.7 19.4 44.1 4 46.2 26.9
42.2 6 50.5 29.2 42.2 ______________________________________
Trial E
0.25 mm. wedge wire perforate member plus labyrinth from elements
of FIG. 6.
______________________________________ Input Output % Hours run
Solids p.p.m. Solids p.p.m. Reduction
______________________________________ 2 30.0 10.8 64.0 4 33.6 7.2
78.6 6 65.2 12.8 80.4 ______________________________________
The results of Trial A are superior to those of Trial D. The
results of Trial B are superior to those of Trial A, C and E. Trial
B gave the best solids reduction.
* * * * *